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WO2009006691A1 - Système et procédé pour distribuer des boissons glacées - Google Patents

Système et procédé pour distribuer des boissons glacées Download PDF

Info

Publication number
WO2009006691A1
WO2009006691A1 PCT/AU2008/001008 AU2008001008W WO2009006691A1 WO 2009006691 A1 WO2009006691 A1 WO 2009006691A1 AU 2008001008 W AU2008001008 W AU 2008001008W WO 2009006691 A1 WO2009006691 A1 WO 2009006691A1
Authority
WO
WIPO (PCT)
Prior art keywords
beverage
orifice
iced
diameter
beer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/AU2008/001008
Other languages
English (en)
Other versions
WO2009006691A8 (fr
Inventor
Benjamin Paul Baker
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tempak International Pty Ltd
Original Assignee
Tempak International Pty Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from AU2007903705A external-priority patent/AU2007903705A0/en
Priority to AU2008274898A priority Critical patent/AU2008274898B2/en
Priority to NZ583213A priority patent/NZ583213A/xx
Priority to DK08772635.2T priority patent/DK2207459T3/da
Priority to EP08772635.2A priority patent/EP2207459B1/fr
Priority to US12/668,138 priority patent/US8464903B2/en
Application filed by Tempak International Pty Ltd filed Critical Tempak International Pty Ltd
Priority to CA2711443A priority patent/CA2711443C/fr
Priority to ES08772635T priority patent/ES2416715T3/es
Priority to PL08772635T priority patent/PL2207459T3/pl
Publication of WO2009006691A1 publication Critical patent/WO2009006691A1/fr
Anticipated expiration legal-status Critical
Publication of WO2009006691A8 publication Critical patent/WO2009006691A8/fr
Ceased legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
    • B67D1/00—Apparatus or devices for dispensing beverages on draught
    • B67D1/08—Details
    • B67D1/0857—Cooling arrangements
    • B67D1/0858—Cooling arrangements using compression systems
    • B67D1/0861—Cooling arrangements using compression systems the evaporator acting through an intermediate heat transfer means
    • B67D1/0865—Cooling arrangements using compression systems the evaporator acting through an intermediate heat transfer means by circulating a cooling fluid along beverage supply lines, e.g. pythons
    • B67D1/0867—Cooling arrangements using compression systems the evaporator acting through an intermediate heat transfer means by circulating a cooling fluid along beverage supply lines, e.g. pythons the cooling fluid being a liquid

Definitions

  • This invention relates to a method of and system for dispensing iced beverages, particularly iced beer and similar alcoholic and/or carbonated ready to drink beverages.
  • chill beers For many years, it has been common to chill beers, lagers and similar beverages in clubs, bars, hotels and other venues from room or cellar temperature, typically around 5 to 15 0 C to somewhere around O 0 C for sale to patrons.
  • the term "beer” should be construed as including any, typically carbonated, and/or relatively low strength alcoholic beverage whether brewed or not. "Beverage” is to include carbonated soft drinks also. Many beverage companies such as brewers, soft and ready to drink manufacturers often require their beverages to be dispensed at a particular temperature or within a particular range of temperatures when sold in bars, hotels or the like.
  • beers are typically required to be sold at a temperature of between 2 and 4 0 C inside the glass, which means that the beer has to be dispensed from the tap in a hotel or bar at around 1° to 2 0 C to allow for the heat capacity of the glass, which will typically be at a temperature greater than 4 0 C.
  • the beer, lager, or the like is typically chilled by a heat exchanger.
  • heat exchangers are usually either installed under a traditional bench or bar top or in the keg cellar, so the size of the heat exchanger is a consideration.
  • the dispensing apparatus must be sufficiently efficient to be able to dispense beer at the correct temperature, as prescribed by the beverage company, and on demand.
  • beer contains alcohol, and is carbonated (under pressure) this depresses the freezing point of the beer such that it freezes at temperatures below the freezing point of water.
  • the stronger the beer in alcohol content the lower the temperature the beer freezes at. Dispensing beers at such low temperatures is tricky and is not possible without an increase in the performance of older type heat exchangers.
  • the present invention provides a method providing an iced beverage, typically alcoholic beverage such as iced beer, or the like, comprising the steps of: dispensing chilled alcoholic beverage from a font or the like, the beverage being at a subzero temperature, typically in the range of minus 2.5 to minus 4.3 0 C; cooling the font to a temperature which is cooler than the beer but not substantially cooler, typically less than one to two degrees cooler than the beverage; wherein the beverage is first dispensed through a smaller orifice of a narrow diameter at a preset low flow rate of beverage, which in turn becomes ice or slush; and after a period of time dispensing the liquid beverage, which may contain ice in the form of seeds, flakes, slush, crystals or the like through a larger diameter orifice.
  • a subzero temperature typically in the range of minus 2.5 to minus 4.3 0 C
  • the beverage is first dispensed through a smaller orifice of a narrow diameter at a preset low flow rate
  • the orifice is partially opened to produce the preset low flow then opened fully substantially immediately after the flow of beverage through the reduced orifice becomes restricted under the low flow rate such that no ice or slush flow is therethrough, which restriction acts as an indicator for the operator to open the tap fully.
  • the opening of the tap to full flow also clears the ice or slush from the small orifice.
  • the heat exchanger is preferably, but need not be, a tubular heat exchanger of the type described in PCT/AU2006/000459.
  • the present invention provides a method providing an iced alcoholic beverage such as iced beer or the like, comprising the steps of supplying the beverage at a pressure of typically about 28 to 36 psi, typically using a mixture of compressed nitrogen and carbon dioxide, and a temperature, typically in the range of 2 to 6 0 C, to a heat exchanger: cooling the beverage in the heat exchanger to a temperature of about -3.6 0 C to - 4.8 0 C; passing the cooled beverage through an orifice (venturi tube) and subsequently into a pipe of increased diameter relative to the orifice thereby creating a venturi effect in the beer line, causing the beverage to thereby release a, preferably predetermined, amount of carbon dioxide from the beverage and cause the production of ice seeds in the beverage; dispensing the chilled beverage from a font or the like, cooled to a temperature which is cooler than the beer but not substantially cooler, typically less than one to two degrees cooler than the beverage; wherein the beverage is first dispensed through a
  • the desired temperature of the beverage on exit from the heat exchanger is set dependant on the alcohol content of the beverage.
  • the orifice has a diameter of 2.5 to 4mm compared with the diameter of the rest of the beverage line of about 8 to 10mm.
  • the venturi tube may be around 100 to 150mm long.
  • the present invention provides a system for providing an iced alcoholic beverage such as iced beer or the like, comprising:- a source of chilled coolant, such as a glycol set, or direct refrigeration Freon system; a beverage line for supplying the alcoholic beverage; a heat exchanger disposed in the beverage line for cooling the alcoholic beverage by heat transfer to the chilled coolant; a restriction or orifice forming a venturi in the beer line downstream from the heat exchanger; a chilled or chillable font for further cooling the beverage downstream from the orifice; and a dispenser tap typically adjacent or part of the font, capable of dispensing the beverage at a relatively low dispense rate and at a relatively higher dispense rate.
  • a source of chilled coolant such as a glycol set, or direct refrigeration Freon system
  • a beverage line for supplying the alcoholic beverage
  • a heat exchanger disposed in the beverage line for cooling the alcoholic beverage by heat transfer to the chilled coolant
  • a restriction or orifice forming a venturi in the
  • the dispenser tap may have two valves one defining a relatively smaller dispense opening and one a relatively larger dispense opening or it may have a single dispense opening which includes a partly closed dispense position and a more fully open dispense setting.
  • Figure 1 is a schematic view of system for dispensing iced beer
  • Figure 2 is a schematic sketch of a beer tap in a partly open position
  • Figure 3 is a schematic sketch of a beer tap in a fully open position
  • Figure 4 is a schematic front view of an alternative beer tap for use in the system and method of the present invention.
  • Figure 1 shows schematically a view of the major components of a system for dispensing iced beer embodying the present invention.
  • Beer flows from a keg 8 or the like in a cellar at a temperature of from 2-6°C along a beverage line or pipe 10, typically having a diameter or 8 to 10mm.
  • a CO 2 driven beverage pump schematically shown at 9, is provided for maintaining a positive back pressure on the beverage line 10.
  • the beverage is typically compressed using both compressed nitrogen and carbon dioxide gases.
  • a typical tap pressure is 5 psi and the pressure range at the cellar may be from 25 to 40 psi, depending on the beverage style.
  • the beer is supplied from the cellar at a pressure of between 28 and 36psi using the mixture of nitrogen and carbon dioxide gases.
  • the pipe is located in an insulated casing 12, only part of which is shown. It is to be noted that typically all cold or cool pipes or components of the system will be insulated, the insulation being omitted from the Figure for reasons of clarity. Also located in the casing are delivery 14 and return 16 pipes carrying chilled coolant (such as glycol) at a temperature of about -5 0 C from a cooler/heat exchanger (known as a "refrigeration set", shown schematically at 16 to a flooded font 18 and back to the refrigeration set for re-cooling the coolant.
  • the beer line 10 passes from the casing 12 to a heat exchanger 20 which may be of the type described in PCT/AU2006/000459, but which could be any other suitable high efficiency compact heat exchanger.
  • the sudden release of carbon dioxide at low beverage dispense rates results in ice seeds being formed in the beer outlet line 10 and supports the production of ice crystals.
  • the beer then passes into the flooded font 18 which defines a volume 19 filled with glycol through which the beer line 10 passes.
  • the beer is dispensed through a two stage beer tap 30 of the type described in Australian provisional application No 2007903705.
  • FIGS. 2 and 3 show a schematic drawing of the two stage beer tap 30 of a beer font 18.
  • the drawings are conceptual and illustrate the principals of operation only which can be implemented using other designs of tap.
  • the beer tap 30 is first only partially opened. How this is achieved is not critical, and the type of valve closing the tap is also not critical. It is also possible to effect the method using an arrangement in which there are two valves, a main pipe and a bypass valve.
  • the diameter of the tap when the valve is fully open is about 6mm, giving an area of about 30mm 2 .
  • the tap may also be partially opened to produce a much reduced low flow rate through an aperture having an effective diameter of about 1.5mm (but which may be in the range of l-2mm) , or an area of 1.75mm 2 .
  • the tap is first only partially opened as shown in Figure 2 to produce a preset small flow through the reduced size aperture. This results in the formation of ice seeds in the pipe 10 within the heat exchanger, as described above due to the pressure drop as the beer exits the orifice 22.
  • Ice slurry or frozen beer 40 is discharged from the tap 30 into a glass 42 or other receptacle under the tap, which continues to flow for a few seconds until the reduced diameter tap orifice becomes restricted with ice. Behind the restriction the beer itself does not freeze as the percentage alcohol content in the liquid phase goes up due to water in the form of ice precipitating out, both as the discharged slush and in the pipe downstream from the tap 10.
  • the reduction of the flow acts as a trigger for the operator to open the tap fully, as shown in Figure 2. ⁇ t this time the opening of the tap fully triggers the flow of sub zero beer which may contain ice crystals into the glass 40 to produce a semi-frozen beer drink.
  • alcoholic and/or carbonated beverages such as lagers, ciders RTDs (mixtures of spirits and soft drinks) having a strength of a few % alcohol, say 2% to about 10%, however, the temperature of the iced drink will vary depending on the strength of the beverage.
  • the method may also be used with non-alcoholic carbonated soft drinks having a high sugar or dissolved salts content, the dissolved sugar/salts depressing the freezing point of the drink.
  • the dispensing of the iced beverage can be achieved by having set positions using a single valve or by having a bypass valve and two flow paths one narrow and one much wider.
  • a dispensing tap having narrow 50 and wider 52 flow paths is shown schematically in Figure 4.

Landscapes

  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Devices For Dispensing Beverages (AREA)
  • Confectionery (AREA)

Abstract

L'invention porte sur un système pour distribuer une boisson alcoolisée glacée, telle qu'une bière glacée ou une boisson non alcoolisée gazeuse. Le système comporte une source de fluide de refroidissement froid (16) et une conduite de boisson (10) pour distribuer la boisson. Un échangeur de chaleur (20) est disposé dans la conduite de boisson (10) pour refroidir la boisson par le transfert de la chaleur au fluide de refroidissement froid. Un étranglement (22) ou un orifice formant un venturi est disposé dans la conduite de boisson (10) en aval de l'échangeur de chaleur. Une source froide (18) pour refroidir encore davantage la boisson est disposée en aval de l'orifice. La source (18) comprend un robinet de distribution (30) pouvant distribuer la boisson à un débit de distribution relativement faible et à un débit de distribution relativement plus élevé. Lors de l'utilisation, la boisson est tout d'abord distribuée à un débit de distribution relativement faible à travers un orifice plus petit d'un diamètre étroit à un débit de boisson faible prédéterminé, et devient de la glace ou de la glace fondante (40). Après une certaine période de temps, la boisson liquide, qui peut contenir de la glace sous la forme de flocons, de glace fondante, de cristaux ou autres, est distribuée à un débit plus rapide, typiquement à travers un orifice de plus grand diamètre.
PCT/AU2008/001008 2007-07-09 2008-07-09 Système et procédé pour distribuer des boissons glacées Ceased WO2009006691A1 (fr)

Priority Applications (8)

Application Number Priority Date Filing Date Title
PL08772635T PL2207459T3 (pl) 2007-07-09 2008-07-09 System i sposób do wydawania chłodzonych lodem napojów
NZ583213A NZ583213A (en) 2007-07-09 2008-07-09 System and method for dispensing iced beverages through different sized orifices
DK08772635.2T DK2207459T3 (da) 2007-07-09 2008-07-09 System og fremgangsmåde til distribution af isafkølede drikkevarer
EP08772635.2A EP2207459B1 (fr) 2007-07-09 2008-07-09 Système et procédé pour distribuer des boissons glacées
US12/668,138 US8464903B2 (en) 2007-07-09 2008-07-09 Method for dispensing iced beverages
AU2008274898A AU2008274898B2 (en) 2007-07-09 2008-07-09 System and method for dispensing iced beverages
CA2711443A CA2711443C (fr) 2007-07-09 2008-07-09 Systeme et procede pour distribuer des boissons glacees
ES08772635T ES2416715T3 (es) 2007-07-09 2008-07-09 Sistema y método para dispensar bebidas heladas

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
AU2007903705A AU2007903705A0 (en) 2007-07-09 Method of dispensing iced beverages
AU2007906039 2007-07-09
AU2007906039A AU2007906039A0 (en) 2007-11-02 Method of dispensing iced beverages
AU2007903705 2007-11-02

Publications (2)

Publication Number Publication Date
WO2009006691A1 true WO2009006691A1 (fr) 2009-01-15
WO2009006691A8 WO2009006691A8 (fr) 2010-08-05

Family

ID=40228114

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/AU2008/001008 Ceased WO2009006691A1 (fr) 2007-07-09 2008-07-09 Système et procédé pour distribuer des boissons glacées

Country Status (9)

Country Link
US (1) US8464903B2 (fr)
EP (1) EP2207459B1 (fr)
AU (1) AU2008274898B2 (fr)
CA (1) CA2711443C (fr)
DK (1) DK2207459T3 (fr)
ES (1) ES2416715T3 (fr)
NZ (1) NZ583213A (fr)
PL (1) PL2207459T3 (fr)
WO (1) WO2009006691A1 (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2389071A1 (es) * 2010-04-16 2012-10-23 Heineken España, S.A. Columna dispensadora de bebidas.
ITMI20121415A1 (it) * 2012-08-08 2014-02-09 Global Fountain S R L Spillatore per bevande
RU2529213C2 (ru) * 2009-01-19 2014-09-27 Найсвенд Лтд. Устройство для розлива с дозированием заказанных замороженных напитков
CN106361147A (zh) * 2015-07-21 2017-02-01 上海匠腾实业有限公司 一种无压步进式热交换饮水装置

Families Citing this family (15)

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DK2207459T3 (da) 2007-07-09 2013-07-08 Tempak Internat Pty Ltd System og fremgangsmåde til distribution af isafkølede drikkevarer
US8678247B2 (en) * 2011-03-31 2014-03-25 Lancer Corporation Creamy foam beer dispensing system
GB201215943D0 (en) * 2012-09-06 2012-10-24 Wickwar Brewing Company Ltd Improvements relating to beverage dispensing
US20140263433A1 (en) * 2013-03-15 2014-09-18 Heineken Uk Limited Beverage Dispense System and Method
GB2519384B (en) * 2013-10-15 2020-07-01 Streamline Beverage Pty Ltd A beverage dispenser
WO2017173495A1 (fr) * 2016-04-06 2017-10-12 Font Fine Wine Pty Ltd Distributeur de boisson
GB201608280D0 (en) * 2016-05-11 2016-06-22 Heineken Uk Ltd Connector
CN105890249A (zh) * 2016-06-08 2016-08-24 何建东 一种快速制冰制雪装置
BE1024348B1 (nl) * 2016-07-01 2018-02-05 Duvel Moortgat Nv Inrichting voor het schenken van bier met hoog koolzuurgehalte
UA113516U (xx) * 2016-10-04 2017-01-25 Комплекс для санітарної обробки і охолодження лінії подачі напою
CZ307071B6 (cs) * 2016-11-08 2017-12-27 Břetislav Matějíček Způsob vytvoření konzistentní granulové zmražené hmoty z alkoholických a nealkoholických nápojů a zařízení k provedení způsobu
US11034569B2 (en) 2018-02-14 2021-06-15 Taphandles Llc Cooled beverage dispensing systems and associated devices
NL2025364B1 (en) 2020-04-17 2021-10-26 Heineken Supply Chain Bv Dispensing supercooled beverage
EP3964767A1 (fr) 2020-09-03 2022-03-09 Heineken Supply Chain B.V. Dispositif de refroidissement d'une boisson comprenant un circuit de refroidissement primaire et secondaire
EP3964474A1 (fr) 2020-09-03 2022-03-09 Heineken Supply Chain B.V. Dispositif de refroidissement d'une boisson comprenant un module tampon

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US4270673A (en) * 1978-07-24 1981-06-02 Alco Foodservice Equipment Company Electric gravity dispensing valve
US4979647A (en) * 1984-06-18 1990-12-25 The Cornelius Company Method and apparatus for cooling and dispensing beverage
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EP1602622A1 (fr) * 2004-06-04 2005-12-07 Whirpool Corporation Distributeur d'eau à débit variable pour réfrigérateurs avec congélateur
US20060045942A1 (en) * 2004-08-31 2006-03-02 Sher Alexander A Method and system for in-cup dispensing, mixing and foaming hot and cold beverages from liquid concentrates

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NZ586788A (en) 2008-01-04 2012-09-28 Tempak Internat Pty Ltd Improvements in heat exchangers for dispensing sub-zero beer where the cooling and beverage lines are embedded in a soild block of material having high thermal conductivity

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GB691569A (en) * 1951-03-19 1953-05-13 Bastian Blessing Co Improvements in or relating to a beverage dispenser and draft arm therefor
US4270673A (en) * 1978-07-24 1981-06-02 Alco Foodservice Equipment Company Electric gravity dispensing valve
US4979647A (en) * 1984-06-18 1990-12-25 The Cornelius Company Method and apparatus for cooling and dispensing beverage
US5086818A (en) * 1989-02-24 1992-02-11 Bendt Larry A Beverage storage and dispensing device
EP1602622A1 (fr) * 2004-06-04 2005-12-07 Whirpool Corporation Distributeur d'eau à débit variable pour réfrigérateurs avec congélateur
US20060045942A1 (en) * 2004-08-31 2006-03-02 Sher Alexander A Method and system for in-cup dispensing, mixing and foaming hot and cold beverages from liquid concentrates

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2529213C2 (ru) * 2009-01-19 2014-09-27 Найсвенд Лтд. Устройство для розлива с дозированием заказанных замороженных напитков
ES2389071A1 (es) * 2010-04-16 2012-10-23 Heineken España, S.A. Columna dispensadora de bebidas.
ITMI20121415A1 (it) * 2012-08-08 2014-02-09 Global Fountain S R L Spillatore per bevande
WO2014024053A1 (fr) * 2012-08-08 2014-02-13 Global Fountain S.R.L. Dispositif de soutirage pour boissons
CN106361147A (zh) * 2015-07-21 2017-02-01 上海匠腾实业有限公司 一种无压步进式热交换饮水装置

Also Published As

Publication number Publication date
DK2207459T3 (da) 2013-07-08
ES2416715T3 (es) 2013-08-02
US8464903B2 (en) 2013-06-18
AU2008274898A1 (en) 2009-01-15
WO2009006691A8 (fr) 2010-08-05
EP2207459A1 (fr) 2010-07-21
EP2207459A4 (fr) 2012-02-08
CA2711443C (fr) 2016-08-30
NZ583213A (en) 2012-10-26
AU2008274898B2 (en) 2014-06-05
EP2207459B1 (fr) 2013-04-10
US20100276443A1 (en) 2010-11-04
PL2207459T3 (pl) 2013-09-30
CA2711443A1 (fr) 2009-01-15

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